JPH0949612A - Air dispersing pipe for fluidizing air - Google Patents

Air dispersing pipe for fluidizing air

Info

Publication number
JPH0949612A
JPH0949612A JP7201204A JP20120495A JPH0949612A JP H0949612 A JPH0949612 A JP H0949612A JP 7201204 A JP7201204 A JP 7201204A JP 20120495 A JP20120495 A JP 20120495A JP H0949612 A JPH0949612 A JP H0949612A
Authority
JP
Japan
Prior art keywords
air
fluidized
outer cylinder
diffuser
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP7201204A
Other languages
Japanese (ja)
Inventor
Masato Ikebe
正人 池辺
Shuhei Ishii
修平 石井
Akira Mochizuki
明 望月
Hideji Mori
秀治 守
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP7201204A priority Critical patent/JPH0949612A/en
Publication of JPH0949612A publication Critical patent/JPH0949612A/en
Pending legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an air dispersing pipe for fluidizing air, which is capable of unifying the outlet temperature of fluidizing air. SOLUTION: This air dispersing pipe for fluidizing air is provided with an outer cylinder 9, whose inlet port side is opened and whose outlet port side is shielded while discharging holes 5 are formed across the whole area in the lengthwise direction of an outer peripheral part, and an inner cylinder 10, retained so as to be fitted loosely into the outer cylinder 9, whose end, opposed to the inlet port side of the outer cylinder 9, is shielded, whose end, opposed to the outlet port side of the outer cylinder 9, is opened and whose small holes 13 are formed across the whole area in the lengthwise direction of the outer peripheral part thereof.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、流動床式ごみ焼却炉に
おいて、流動媒体を流動化させる流動化空気用散気管に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air diffuser for fluidized air for fluidizing a fluid medium in a fluidized bed refuse incinerator.

【0002】[0002]

【従来の技術】従来、流動床式ごみ焼却炉において、流
動床を形成するために、高温の流動空気を散気管に供給
して、吐出孔より吐出を行い、流動媒体を活性化して流
動床を形成していた。
2. Description of the Related Art Conventionally, in a fluidized bed type refuse incinerator, in order to form a fluidized bed, high temperature fluidized air is supplied to an air diffuser and discharged from a discharge hole to activate a fluidized medium to activate the fluidized bed. Had formed.

【0003】図5は従来例に係る散気管の構成図であ
り、同図(a)は側面図、同図(b)は一部断面正面図
である。
FIG. 5 is a configuration diagram of an air diffuser according to a conventional example. FIG. 5 (a) is a side view and FIG. 5 (b) is a partially sectional front view.

【0004】散気管4において、外筒12の散気管入口
7より流動空気の供給を行う。この空気は、散気管出口
側に閉止フランジ8が設けてあり遮蔽されていることか
ら、外筒12に形成された吐出孔5より管外へ吐出され
る。
In the air diffuser 4, flowing air is supplied from the air diffuser inlet 7 of the outer cylinder 12. This air is discharged to the outside of the pipe from the discharge hole 5 formed in the outer cylinder 12, because the closing flange 8 is provided on the outlet side of the air diffusing pipe and is shielded.

【0005】[0005]

【発明が解決しようとする課題】上記従来技術は、流動
床式ごみ焼却設備において、流動床を形成する設備とし
て散気管を用いているが、通常250〜300℃の流動
空気を供給している一方、散気管を取り巻く流動媒体の
温度は700〜800℃と高いため、散気管外壁を通し
て熱交換が行われ、吹き出し流動空気温度は、散気管の
手前側では低く奥側では高くなり、温度差が生じるた
め、下記のような問題があった。
In the above-mentioned prior art, in the fluidized bed type refuse incinerator, the air diffuser is used as the equipment for forming the fluidized bed, but normally the fluidized air at 250 to 300 ° C. is supplied. On the other hand, since the temperature of the fluid medium surrounding the diffuser pipe is as high as 700 to 800 ° C, heat exchange is performed through the outer wall of the diffuser pipe, and the temperature of the blown flowing air is low on the front side of the diffuser pipe and high on the back side. Therefore, there are the following problems.

【0006】(1)流動床を形成するに当たり、前記吐
出孔が同一口径とすると流動空気が高温となるほど吹き
出し速度が速くなり流動床は活性化するが、散気管内で
熱交換を行い部分的に温度差が生じると、均一な流動床
は形成できなくなる。
(1) In forming a fluidized bed, if the discharge holes have the same diameter, the higher the temperature of the fluidized air, the faster the blowing rate and the activated fluidized bed. If there is a temperature difference between the two, a uniform fluidized bed cannot be formed.

【0007】(2)250〜300℃の流動空気を散気
管に供給した場合、奥側に行くほど散気管内で熱交換を
行って吹き出し温度は高温となるため、散気管外壁も高
温となり高温腐食が発生し易くなり、散気管の寿命は短
くなる。
(2) When flowing air of 250 to 300 ° C. is supplied to the air diffuser, heat is exchanged in the air diffuser as it goes deeper and the blowout temperature becomes higher, so that the outer wall of the air diffuser also becomes hot. Corrosion is likely to occur and the life of the air diffuser is shortened.

【0008】本発明の目的は、上記従来技術の欠点を解
消し、流動空気の吹き出し温度を均一化させることがで
きる流動化空気用散気管を提供することにある。
An object of the present invention is to solve the above-mentioned drawbacks of the prior art and to provide a diffuser tube for fluidized air which can make the blowing temperature of the fluidized air uniform.

【0009】[0009]

【課題を解決するための手段】上記目的を達成するため
に、第1の手段は、入口側を開口すると共に出口側を遮
蔽し、かつ、外周部の長手方向全域に亘って吐出孔を形
成し、入口から供給される流動空気と、この流動空気よ
り高温の外部の流動媒体との間で熱交換を行って、高温
化した流動空気を吐出孔より吐出する流動化空気用散気
管において、入口側を開口すると共に出口側を遮蔽し、
かつ、外周部の長手方向全域に亘って吐出孔を形成した
外筒と、この外筒に遊嵌されるように保持されると共
に、外筒の入口側と対面する端部が遮蔽され、かつ、外
筒の出口側と対面する端部が開口し、さらに外周部の長
手方向全域に亘って小孔が形成された内筒とを備えてい
ることを特徴とする。
In order to achieve the above object, the first means is to open an inlet side and shield an outlet side, and to form a discharge hole over the entire length of the outer peripheral portion in the longitudinal direction. Then, in the air diffuser for fluidized air that performs heat exchange between the fluidized air supplied from the inlet and an external fluidized medium having a temperature higher than that of the fluidized air, and discharges the fluidized air having a high temperature from the discharge hole, Open the entrance side and shield the exit side,
Moreover, the outer cylinder having discharge holes formed in the entire length of the outer peripheral portion in the longitudinal direction, and the outer cylinder held so as to be loosely fitted to the outer cylinder, and the end portion facing the inlet side of the outer cylinder is shielded, and An inner cylinder having an opening at an end facing the outlet side of the outer cylinder and further having a small hole formed over the entire length of the outer circumference in the longitudinal direction is characterized.

【0010】また第2の手段は、入口側を開口すると共
に出口側を遮蔽し、かつ、外周部の長手方向全域に亘っ
て吐出孔を形成し、入口から供給される流動空気と、こ
の流動空気より高温の外部の流動媒体との間で熱交換を
行って、高温化した流動空気を吐出孔より吐出する流動
化空気用散気管において、外周部に、吐出孔と対面する
部分を開口した耐火材を設けたことを特徴とする。
The second means is such that the inlet side is opened and the outlet side is shielded, and the discharge hole is formed over the entire area of the outer peripheral portion in the longitudinal direction, and the flowing air supplied from the inlet and the flowing air. In a diffuser tube for fluidized air that discharges hot fluidized air from a discharge hole by exchanging heat with an external fluid medium having a temperature higher than that of air, a portion facing the discharge hole is opened on the outer peripheral portion. The feature is that a refractory material is provided.

【0011】[0011]

【作用】第1の手段においては、散気管外筒壁を通し
て、流動媒体の保有熱と、散気管外筒および内筒間に流
れる流動空気との間で熱交換を行った後、この流動空気
を散気管内筒に流すようにする。従って、散気管外筒と
散気管内筒の温度差は少なくなり、散気管内筒での熱交
換量も少なくなり、流動空気の吹き出し温度は高温均一
となる。その結果、吹き出し温度も均一となって安定し
た流動床が形成できる。
In the first means, heat is exchanged between the retained heat of the fluid medium and the flowing air flowing between the outer tube and the inner tube of the diffuser pipe through the wall of the diffuser pipe outer cylinder, and then the flowing air. To the inner tube of the air diffuser. Therefore, the temperature difference between the outer tube of the air diffusing tube and the inner tube of the air diffusing tube is small, the amount of heat exchange in the inner tube of the air diffusing tube is also small, and the temperature of blowing the flowing air is high. As a result, the blowing temperature becomes uniform and a stable fluidized bed can be formed.

【0012】また、散気管の手前側と奥側での吹き出し
温度勾配が少ないため、流動媒体の局所的な低温域、高
温域が少なくなり、焼却条件の均一化が図れる。
Further, since the blowing temperature gradient on the front side and the back side of the air diffuser is small, the local low temperature region and high temperature region of the fluidized medium are reduced, and the incineration conditions can be made uniform.

【0013】また、散気管内で熱交換を行い流動空気の
吹き出し温度を高温均一とすることができるため、散気
管に供給される流動空気の温度は従来の温度に比べ下げ
ることができる。この結果、散気管外壁の低温化が図れ
るので高温腐食による短寿命の問題もクリアできる。
Further, since the temperature of the blowing air of the flowing air can be made uniform at a high temperature by exchanging heat in the diffusing tube, the temperature of the flowing air supplied to the diffusing tube can be lowered as compared with the conventional temperature. As a result, the temperature of the outer wall of the air diffuser can be lowered, and the problem of short life due to high temperature corrosion can be solved.

【0014】第2の手段においては、散気管に耐火材を
設けることにより、熱交換量が少なくなり流動空気の温
度が均一となるため、上記と同様の作用が得られる。
In the second means, by providing a refractory material in the air diffuser, the amount of heat exchange is reduced and the temperature of the flowing air becomes uniform, so that the same effect as above can be obtained.

【0015】[0015]

【実施例】以下、本発明の各実施例を図面に基づいて説
明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0016】図1は本発明が適用される流動床式ごみ焼
却設備の全体構成図である。
FIG. 1 is an overall configuration diagram of a fluidized bed type refuse incineration facility to which the present invention is applied.

【0017】図1に示すシステムでは、流動ブロワ1よ
り大気の吐出を行い、空気予熱器2で流動空気の温度を
約250〜300℃に上げて、散気管ヘッダ3にこの高
温空気の供給を行うようになっている。
In the system shown in FIG. 1, the air is discharged from the fluid blower 1, the temperature of the fluid air is raised to about 250 to 300 ° C. by the air preheater 2, and the hot air is supplied to the air diffuser header 3. I am supposed to do it.

【0018】そして、各々の散気管4を通して、吐出孔
5より流動媒体6へ高温空気の吐出を行い、流動床が形
成されるようになっている。
Then, high temperature air is discharged from the discharge holes 5 to the fluid medium 6 through each air diffuser 4 to form a fluidized bed.

【0019】図2は第1の実施例に係る散気管の構成図
であり、同図(a)は側面図、同図(b)は一部縦断正
面図である。
FIG. 2 is a configuration diagram of an air diffusing tube according to the first embodiment, FIG. 2 (a) is a side view, and FIG. 2 (b) is a partially longitudinal front view.

【0020】図2に示す第1の実施例に係る散気管4
は、入口側を開口すると共に出口側を閉止フランジ8で
遮蔽し、かつ、外周部の長手方向全域に亘って吐出孔5
を形成した外筒9と、この外筒9に遊嵌されるように保
持されると共に、外筒9の入口側と対面する端部が閉止
フランジ11で遮蔽され、かつ、外筒9の出口側と対面
する端部が開口し、さらに外周部の長手方向全域に亘っ
て小孔13が形成された内筒10とを備えている。
The air diffuser 4 according to the first embodiment shown in FIG.
Is opened on the inlet side and is closed on the outlet side by the closing flange 8, and the discharge hole 5 is formed over the entire area in the longitudinal direction of the outer peripheral portion.
And an outer cylinder 9 formed with the outer cylinder 9, the end of the outer cylinder 9 facing the inlet side is shielded by the closing flange 11, and the outlet of the outer cylinder 9 is retained. The inner cylinder 10 is provided with an opening at an end facing the side and further having a small hole 13 formed over the entire area of the outer peripheral portion in the longitudinal direction.

【0021】このような構成において、入口7より流動
空気の供給を行った時、この空気が外筒9と内筒10の
間を通る途中に、外筒壁を通して、流動媒体6の保有熱
により熱交換が行われる。
In such a structure, when the flowing air is supplied from the inlet 7, while the air passes between the outer cylinder 9 and the inner cylinder 10, it is passed through the outer cylinder wall by the heat retained by the fluid medium 6. Heat exchange takes place.

【0022】散気管出口側に閉止フランジ8を設けてい
るので、流動空気は内筒10の内部に供給されるが、内
筒出口側にも閉止フランジ11を設けているので、この
流動空気は小孔13から内筒10と外筒9の隙間に流出
し、さらに吐出孔5より管外へ吐出される。
Since the closing flange 8 is provided on the air diffuser outlet side, the flowing air is supplied to the inside of the inner cylinder 10. However, since the closing flange 11 is also provided on the inner cylinder outlet side, the flowing air is It flows from the small hole 13 into the gap between the inner cylinder 10 and the outer cylinder 9, and is further discharged from the discharge hole 5 to the outside of the pipe.

【0023】この時、内筒10内に供給された流動空気
は、外筒9と内筒10の間と、内筒10内の温度差が少
ないため、熱交換が行われず、流動空気の吹き出し温度
は高温均一となり、吐出孔5を通して流動媒体6へ吐き
出される吹き出し速度も均一となって安定した流動床が
形成できる。
At this time, the flowing air supplied into the inner cylinder 10 has a small temperature difference between the outer cylinder 9 and the inner cylinder 10 and inside the inner cylinder 10, so that heat exchange is not performed and the flowing air is blown out. The temperature becomes uniform at a high temperature, and the blowing speed of the gas discharged to the fluid medium 6 through the discharge holes 5 becomes uniform, so that a stable fluidized bed can be formed.

【0024】また、散気管4の入口側と奥側での吹き出
し温度が高温均一となるので、温度勾配が少なくなり、
流動媒体6の局所的な低温域、高温域が少なくなり、焼
却条件の均一化を図ることができる。
Further, since the blowing temperatures on the inlet side and the inner side of the air diffuser 4 are high in temperature, the temperature gradient is reduced,
The local low temperature region and high temperature region of the fluidized medium 6 are reduced, and the incineration conditions can be made uniform.

【0025】また、外筒9と内筒10の間で、散気管外
壁を通して流動媒体6の保有熱により熱交換が行われる
ことを考慮した場合、図3に記したように、高温腐食は
320℃から急激に起こり易くなるので、流動空気の温
度を320℃以下に設定する。
Considering that heat is exchanged between the outer cylinder 9 and the inner cylinder 10 through the outer wall of the air diffusing pipe by the retained heat of the fluidized medium 6, as shown in FIG. The temperature of the flowing air is set to 320 ° C. or lower because it tends to occur rapidly from 0 ° C.

【0026】そのため、入口7に供給される流動空気は
従来の温度よりも下げることができるので、散気管外壁
が高温腐食を起こすことがなくなり、散気管4の寿命は
延びる。
Therefore, the flowing air supplied to the inlet 7 can be cooled to a temperature lower than the conventional temperature, so that the outer wall of the air diffuser tube is not corroded at high temperature, and the life of the air diffuser tube 4 is extended.

【0027】ここで、内筒10の材質を、耐熱性、断熱
性がある材質(例えばセラミック等)にすれば、吹き出
し温度はより高温均一となって安定した流動床を形成で
きる。
Here, if the material of the inner cylinder 10 is made of a heat-resistant and heat-insulating material (such as ceramic), the blowing temperature becomes even higher and a stable fluidized bed can be formed.

【0028】図4は第2の実施例に係る散気管4の構成
図であり、同図(a)は側面図、同図(b)は一部縦断
正面図である。
FIG. 4 is a configuration diagram of the air diffusing tube 4 according to the second embodiment. FIG. 4 (a) is a side view and FIG. 4 (b) is a partially longitudinal front view.

【0029】図4に示す第2の実施例に係る散気管4
は、外筒9の単一筒体とし、かつその外周部に耐火材1
4を設けたものである。耐火材14において、外筒9に
形成された吐出孔5と対向する個所には開口が形成され
ており、流動空気の吐出に差し支えないようになってい
る。
The air diffuser 4 according to the second embodiment shown in FIG.
Is a single cylinder of the outer cylinder 9, and the refractory 1
4 is provided. An opening is formed in the refractory material 14 at a position facing the discharge hole 5 formed in the outer cylinder 9 so that the discharge of the flowing air may be prevented.

【0030】このように、耐火材14を設けることによ
り、熱交換量が少なくなり、流動空気の温度を均一にす
ることができるため、第1の実施例と同様の効果が得ら
れる。
By providing the refractory material 14 in this way, the amount of heat exchange is reduced and the temperature of the flowing air can be made uniform, so that the same effect as in the first embodiment can be obtained.

【0031】[0031]

【発明の効果】請求項1記載の発明によれば、散気管の
構造を二重管構造とし、散気管外筒壁を介して流動媒体
と流動空気を熱交換させ、散気管内筒に流すことにより
流動空気の温度が高温均一となるため、散気管の吹き出
し温度が一定となり、流動床の流動状態を安定化させる
ことができる。
According to the first aspect of the present invention, the structure of the air diffusing tube is a double tube structure, and the flowing medium and the flowing air are heat-exchanged through the outer tube wall of the air diffusing tube and flow into the inner tube of the air diffusing tube. As a result, the temperature of the fluidized air becomes high in temperature, so that the blowing temperature of the air diffuser becomes constant, and the fluidized state of the fluidized bed can be stabilized.

【0032】また、散気管の手前側と奥側での吹き出し
温度勾配が少ないため、流動媒体の局所的な低温域、高
温域が少なくなり、焼却条件の均一化を図ることができ
る。さらに、散気管へ供給する流動空気の温度を下げる
ことにより散気管に高温腐食が発生しにくくなるので、
散気管の長寿命化が達成できる。
Further, since the blowing temperature gradient on the front side and the back side of the air diffuser is small, the local low temperature region and high temperature region of the fluidized medium are reduced, and the incineration conditions can be made uniform. Furthermore, by lowering the temperature of the flowing air supplied to the diffuser pipe, high temperature corrosion is less likely to occur in the diffuser pipe,
The life of the air diffuser can be extended.

【0033】請求項2記載の発明によれば、耐火材によ
り、熱交換量を少なくし流動空気の温度を均一にするこ
とができるため、上記と同様の効果を奏することができ
る。
According to the second aspect of the present invention, the refractory material can reduce the heat exchange amount and make the temperature of the flowing air uniform, so that the same effect as described above can be obtained.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明が適用される流動床式ごみ焼却設備の全
体構成図である。
FIG. 1 is an overall configuration diagram of a fluidized bed waste incineration facility to which the present invention is applied.

【図2】本発明の第1の実施例に係る散気管の構成図で
ある。
FIG. 2 is a configuration diagram of an air diffusing tube according to the first embodiment of the present invention.

【図3】管壁温度と腐食速度の関係を示す特性図であ
る。
FIG. 3 is a characteristic diagram showing a relationship between a tube wall temperature and a corrosion rate.

【図4】本発明の第2の実施例に係る散気管の構成図で
ある。
FIG. 4 is a configuration diagram of an air diffusing tube according to a second embodiment of the present invention.

【図5】従来例に係る散気管の構成図である。FIG. 5 is a configuration diagram of an air diffuser according to a conventional example.

【符号の説明】[Explanation of symbols]

5 吐出孔 9 外筒 10 内筒 13 小孔 14 耐火材 5 Discharge hole 9 Outer cylinder 10 Inner cylinder 13 Small hole 14 Refractory material

───────────────────────────────────────────────────── フロントページの続き (72)発明者 望月 明 広島県呉市宝町6番9号 バブコツク日立 株式会社呉工場内 (72)発明者 守 秀治 神奈川県横浜市磯子区磯子1丁目2番10号 バブコツク日立株式会社横浜エンジニア リングセンタ内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Akira Mochizuki 6-9 Takara-cho, Kure City, Hiroshima Prefecture Bab Kotsk Hitachi Co., Ltd. Kure Factory (72) Inventor Hideharu Mori 1-2-10 Isogo, Isogo-ku, Yokohama-shi, Kanagawa Prefecture Babkotsu Hitachi Co., Ltd. Yokohama Engineering Center

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 入口側を開口すると共に出口側を遮蔽
し、かつ、外周部の長手方向全域に亘って吐出孔を形成
し、入口から供給される流動空気と、この流動空気より
高温の外部の流動媒体との間で熱交換を行って、高温化
した流動空気を吐出孔より吐出する流動化空気用散気管
において、 入口側を開口すると共に出口側を遮蔽し、かつ、外周部
の長手方向全域に亘って吐出孔を形成した外筒と、この
外筒に遊嵌されるように保持されると共に、外筒の入口
側と対面する端部が遮蔽され、かつ、外筒の出口側と対
面する端部が開口し、さらに外周部の長手方向全域に亘
って小孔が形成された内筒とを備えていることを特徴と
する流動化空気用散気管。
1. A fluidized air supplied from an inlet, and an exterior having a temperature higher than that of the fluidized air, wherein the inlet side is opened and the outlet side is shielded, and a discharge hole is formed over the entire area of the outer peripheral portion in the longitudinal direction. In the diffuser pipe for fluidized air that exchanges heat with the fluidized medium of the above, and discharges the heated fluidized air from the discharge hole, the inlet side is opened and the outlet side is shielded, and the length of the outer peripheral portion is long. An outer cylinder having discharge holes formed over the entire direction, and an outer cylinder that is held so as to be loosely fitted to the outer cylinder, has its end facing the inlet side of the outer cylinder shielded, and has an outlet side of the outer cylinder. An air diffuser for fluidized air, comprising: an inner cylinder having an end portion facing the opening and an inner cylinder having a small hole formed in the entire outer peripheral portion in the longitudinal direction.
【請求項2】 入口側を開口すると共に出口側を遮蔽
し、かつ、外周部の長手方向全域に亘って吐出孔を形成
し、入口から供給される流動空気と、この流動空気より
高温の外部の流動媒体との間で熱交換を行って、高温化
した流動空気を吐出孔より吐出する流動化空気用散気管
において、 外周部に、吐出孔と対面する部分を開口した耐火材を設
けたことを特徴とする流動化空気用散気管。
2. A flow air supplied from the inlet and an outside having a temperature higher than that of the flow air, the inlet side being opened and the outlet side being shielded, and the discharge hole being formed over the entire area in the longitudinal direction of the outer peripheral portion. In the air diffuser for fluidized air that exchanges heat with the fluidized medium of the above, and discharges the heated fluidized air from the discharge hole, a refractory material with an opening facing the discharge hole is provided on the outer periphery. An air diffuser for fluidized air.
JP7201204A 1995-08-07 1995-08-07 Air dispersing pipe for fluidizing air Pending JPH0949612A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7201204A JPH0949612A (en) 1995-08-07 1995-08-07 Air dispersing pipe for fluidizing air

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7201204A JPH0949612A (en) 1995-08-07 1995-08-07 Air dispersing pipe for fluidizing air

Publications (1)

Publication Number Publication Date
JPH0949612A true JPH0949612A (en) 1997-02-18

Family

ID=16437080

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7201204A Pending JPH0949612A (en) 1995-08-07 1995-08-07 Air dispersing pipe for fluidizing air

Country Status (1)

Country Link
JP (1) JPH0949612A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100935302B1 (en) * 2008-05-06 2010-01-06 한국수자원공사 A bubble washing device for submerged type micro-filtration membrane using double pipe

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07190065A (en) * 1993-12-27 1995-07-28 Sutaaraito Kogyo Kk Sliding member
JPH11209640A (en) * 1998-01-19 1999-08-03 Starlite Co Ltd Synthetic resin molding excellent in frictional and abrasion characteristic and its production
JP2002265522A (en) * 2001-03-09 2002-09-18 Kurabo Ind Ltd Method of improving pra resin

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07190065A (en) * 1993-12-27 1995-07-28 Sutaaraito Kogyo Kk Sliding member
JPH11209640A (en) * 1998-01-19 1999-08-03 Starlite Co Ltd Synthetic resin molding excellent in frictional and abrasion characteristic and its production
JP2002265522A (en) * 2001-03-09 2002-09-18 Kurabo Ind Ltd Method of improving pra resin

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100935302B1 (en) * 2008-05-06 2010-01-06 한국수자원공사 A bubble washing device for submerged type micro-filtration membrane using double pipe

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